14 Nov 2013

CBI World Group Connected To Regional Partner Hammam Industries & Co. Egypt.

- Welcome To CBI World Click Here To See Intro"
or view CBI Group Intro by clicking here'

- Visit or Email Hammam Industries & Co. Engineering Staff Egypt for Regional Supplier & Manufacturer for Original CBI Equipment & Spare Service Parts including Maintenance"

- For the latest Innovation & Technology Visit The CBI Group Today for further product design information"
Visit Hammam Industries & Co. Egypt For Regional Components & Products Maintenance Service & Spare parts provider see the range of Hammam - CBI Fans view product complete description on environmental expert for tested & certified CBI fans.
CBI Group
- Visit Masters of The Wind Web Page for Further Details" 


Email HAMMAM Supplier of CBI - CB JET Axial Fans in EGYPT & Regional Area For Tunnel Ventilation Application Inquires, Or View Installation, Use & Maintenance Manual Below or click link to download pdf. file;



View Our Related Hi Article Posts on Hi Wise Products Blog on further reading for;

1-  Click to view Post on CBI Group includes Product range & information Catalog.  

2- Click to view Post on Hi Industrial Energy Management - Fans & Blowers. Includes a information on fan optimization FAQ & a download link available to the free Fan Assessment Tool FSAT this helps quantify the potential benefits of optimizing fan system configurations that serve industrial processes.

3- Click to view Post on Hi Ventilating Giant Railway Tunnels, feature free access to The Tunneling Portal for ventilation calculations & further reading on advances on acoustics & vibration. 

Email Hammam Industries & Co Engineering Staff


6 Nov 2013

Hi Leeds Green Cooling Towers Products.

Why use recycled Water?


In today’s highly competitive markets, businesses and institutions must make wise use of available resources. Increasingly the most forward-thinking companies are partnering with local utilities to reduce their demands for energy and water, both to save costs and improve the long-term sustainability of their business.

Using highly treated recycled water for non-potable purposes is an effective way to reduce the demand for precious fresh-water resources. It is also a recognized green building practice. Recycled water has been used in industrial settings throughout California and the arid west for nearly 100 years. 

Locally, Biogen Idec, a company specializing in the development of therapeutic products for the medical field, worked with the County and City of San Diego in 2006 to convert their cooling towers to recycled water. The cooling towers at Biogen Idec are the largest users of water in the facility. 

Conversion to recycled water has allowed Biogen Idec to realize significant cost savings through discounted rates and has provided Biogen Idec with a drought-proof source of water. Elsewhere in Southern California, Orange County’s Irvine Ranch Water District provides recycled water for cooling tower and toilet-flushing use in over 40 high-rise office buildings. Los Angeles County’s West Basin Municipal Water District delivers service to the cooling towers at Cal State Dominguez Hills and the American Honda Campus. 



In Riverside County, Inland Empire Utilities Agency’s headquarters building secured 52 LEED® points to achieve Platinum Certification from the U.S. Green Building Council. Among these points was credit in the “Innovation and Design Process” category because of indoor recycled water use. There is approximately 13,000 acre-feet of recycled water reused annually within the San Diego County Water Authority (SDCWA) service area. Roughly 70% of the recycled water is used for agriculture, landscape irrigation, and other municipal and industrial uses. The annual beneficial reuse of recycled water in San Diego County is projected to increase to over 53,000 acre-feet by the year 2020. By converting to recycled water, cooling tower customers can secure a drought-proof water supply that can protect future growth potential even when water supply shortages loom. Converting to recycled water enhances overall water use efficiency and helps customers comply with their green building goals.

Operational road map to converting cooling towers




The steps for establishing an operational regime for a cooling tower are outlined below. These steps can be performed by the system owner or, as is often the practice, by its maintenance contractor.

Step 1: Determine the materials used in the cooling system and the temperature, flow rates and hours of operation. By understanding these factors, system owners can narrow the list of water quality constituents that cause concern. For example, if a system contains 304 SS, chloride levels are an important concern. However if the system is constructed of fiberglass, this water quality parameter is less of a problem.

Step 2: Evaluate the source water quality in order to understand if treatment is necessary to make the water compatible with your system materials.

Step 3: Select a treatment system if source quality is problematic. 

Step 4: Establish the desired cycles of concentration to minimize water and chemical use, without compromising system performance. While pretreatment can condition water to acceptable standards, each cycle of concentration will increase the TDS, Conductivity and Chlorine concentration in the water and at some point, these constituents will affect system performance. This point limits the cycles of concentration and establishes when blow-down should occur and make-up water added. The system manufacturer’s recommendations for conductivity and system performance with respect to TDS will likely be the limiting factors on cycles of concentration.

Step 5: Potable water back-up is necessary. This will provide increased reliability and assist with blending during conversion.

Step 6: Monitor Makeup and Blow-down water quality to confirm that the system is behaving as 
anticipated.

Step 7: Reset chemical dosing and/or cycles of concentration as necessary to achieve desired performance.

Further Reading on Cooling Tower Resources:

Click image above to Visit MESAN Group Website to View CTI certified Cooling Towers or Visit Hammam Industries & Co. your local supplier in Egypt. 

 Visit Hammam Industries & Co. Supplier of Mesan Group CTI Cooling Towers in Egypt
Click Image Above to visit Hammam Industries & Co. CTI Mesan Product Range in Egypt

The following resources provide more guidance on water best management practices.

28 Oct 2013

Hi Cooling Tower Water Efficiency.

Ways to improve water efficiency.


There are four areas where cooling tower water consumption can be reduced:

1) Evaporation:

Evaporative cooling is integral to open loop cooling towers, accounting for around 86% of cooling tower water consumption (AIRAH, 2010) and cannot be significantly reduced without degrading the cooling tower’s performance. However, locating the system in a hot and windy position will increase water waste. By reducing the heat load on the cooling tower using a dry or closed loop system, the evaporative cooling work can be reduced.

2) Blow-down

Blow-down water is a vital process to preserve long life and efficiency of equipment as it reduces the build up of solids (salts, dirt, calcium, rust) in the system. The frequency of blow-down discharge is typically monitored by measuring cooling water conductivity. Water consumption can be reduced by:

• Improving the quality of feed water
• Optimizing the cooling tower process, and
• Removing solids from blow-down water before

Recirculating this water into the system. It is possible to reduce blow-down volume without compromising plant longevity and efficiency by automating blow-down based on the conductivity of the circulating water to maintain the maximum allowable solids/conductivity (while staying within system requirements).

3) Reuse of Blow-down

A growing number of companies are now collecting blow-down water for reuse onsite instead of using
potable water. Blow-down water is typically higher in dissolved solids but can be (provided there are no harmful chemical treatments or risks of biological contamination) used for:

• wash down
• cleaning, and
• toilet flushing.

Depending on the types of plants and grasses in the gardens blow-down water can be used to offset or replace irrigation water. [It is wise to test this water on a small section of the gardens to see if there are any negative effects.] Blow-down can also be deionised and reused in the cooling circuit [provided there is chemical compatibility].

4) Drift, Splash-out, overflow and other losses

Cooling tower efficiency can be improved by locating the tower in areas not exposed to high winds or excessive heat. Winds can cause spray drift and splash out from air inlets. Design features such as drift eliminators or internal walls will reduce water loss in open loop cooling towers. In some cases, drift from the cooling towers may pose a public health issue. Overflow can happen when a poorly adjusted float valve (or bad design) lets the tower overfill until water flows straight out the overflow and into the sewer. This problem can be avoided by checking during routine maintenance and by monitoring water consumption. Overflow water can also be diverted to storage for reintroduction either with or without processing for use in the make-up water. Make-up water is the water added to compensate for all the water losses through the system. The more efficient the system the less make up water required. Leaks can be detected either by inspection, performing a mass balance or direct metering of flows. Leaks, however small in appearance, can be significant, in some cases 30% of a company’s water usage.


Checklist of Water Efficiency Improvements


1 - Calculate cooling tower water efficiency using the cooling tower water efficiency calculator.
2 - Determine a baseline and compare with industry benchmarks. This will also help assess the success of each water saving action.
3 - Ensure make up water valves and overflow valves are correctly set.
4 - Eliminate all leaks and monitor consumption.
5 - Check if make-up water can be replaced with recycled, rain or storm water feeds.
6 - Improve plant design, location and environment to optimize efficiency.
7 - Pre-cool water with a dry heat ex-changer to reduce heat load on cooling tower (hybrid systems).
8 - Improve plant design to eliminate overflow, splash-out, and drift.
9 - Continuously monitor blow-down water to maintain a higher average conductivity, thus reducing total blow-down.
10 - Investigate and implement recycling blow-down for reuse.

*References: AIRAH, Dec 2010, Cooling system water efficiency study project report.

27 Oct 2013

Hi Ventilating Giant Railway Tunnels (Spain).


Concepts of Tunnel Ventilation and Fire & Life Safety Systems;

The ventilation design of a metro or railway tunnel system requires broad know-how in various fields: from profound knowledge in aero- and thermodynamics and the capability to perform simulations of complex tunnel systems to the implementation of the design into operational, reliable ventilation systems.



Ventilation calculation
Click Here To Access The Tunneling Portal

The ventilation calculation on the internet according to the internationally renowned Swiss standard SIA 196 for the tunnel construction and mining. 

Features:


- online and always available
- calculation of all necessary ventilation parameters
- proposal of the appropriate duct diameter
- proposal of the appropriate fan
- save, edit and copy calculations
- calculations managed in folders
- calculations are protected and can be viewed
  only with member access
- free, no fees




Advances in Acoustics and Vibration;


21 Oct 2013

Hi Water Conservation in Cooling Towers!.

BEST PRACTICE GUIDELINES!.




An insight fully informative & simplified document overview on water conservation in Cooling Towers by the Australian Institute of Refrigeration, Air Conditioning & Heating.






MESAN Group CTI Certified Cooling Towers
For more than 30 years, MESAN Group has engaged in designing, manufacturing and servicing cooling towers, and is supplying air-conditioning to the industrial, refrigeration and HVAC markets. Headquartered in Hong Kong with offices and factory in Mainland China as well as distribution network across the globe.
MESAN Cooling Towers Ltd. are designed to meet the thermal performance, energy saving, environmental friendliness with best performing, proven and innovative solutions. Today, MESAN continues to play a vital role in the development of cooling towers and are proud to have been selected as a key supplier for many of the renowned projects all over the world.
Mesan Fiberglass Engineering (International) Ltd is an Authorized Distributor of Daikin Air Conditioning Units from Japan and the Sole Distributor for Sung Il GRP Water Tanks from Korea. Nowadays MESAN Group offers market expertise in the areas of manufacturing, sales, marketing , distribution and services of HVAC products. From a single source provider to a turnkey project, Mesan provides the engineering expertise to provide optimum cooling to every application. 
Contact Hammam Industries & Co. Egypt for Regional MESAN Group CTI Certified Cooling Tower Supplier & Supplier of PEP Filters USA for Cooling Towers Filtration or Visit Hammam Industries & Co. Website.

9 Oct 2013

Hi PEP FILTERS for "Advanced Filtration Solutions."

Hammam Industries & Co. Egypt's Regional Supplier of PEP FILTERS Advanced filtration solutions manufacturing automatic self cleaning filters. World leader of  of process water filtration ,cooling tower filtration & membrane pre-filtration, & more...,



Click Here To Visit PEP FILTERS Web Site or Click to Email Hammam Industries & Co. For Inquiries in Egypt.  

PEP Highlight from Technical Library;
Benefits of clean water; 


How to Keep HVAC Condensing Water Systems Free from Contamination.




*Please Visit PEP Web Site for Complete Technical Library information access.


20 Apr 2013

Hi Industrial Energy Management - Cooling Water System (Section 2).



Complete this questionnaire to better characterize your equipment condition and energy savings opportunities. If an energy savings opportunity is identified, the results will appear immediately below the question.
Yes / No?

  • Do you regularly (quarterly or more frequently) inspect the cooling water system, and do you frequently monitor cooling water exchanger fouling rates and/or pressure drops?
  • Do cooling water basin temperatures approach within 5 °F of wet bulb temperature, do you have higher-than-design cooling loads, or do you have sludge or sediment problems in cooling tower basins?
  • Are the cooling tower fans controlled only by manual on/off switches? 
  • Do you have a strong cooling water equipment maintenance program?

General Suggestions

Consider the following general recommendations regarding steps that can be taken on a regular basis to help keep refrigeration systems running properly and efficiently:
  1. Report and repair any pipes that are vibrating.
  2. Make sure the control settings for the refrigeration system are easy to find and interpret for ease of system tuning and adjustment.
  3. Keep the doors to cold storage areas closed whenever possible.
  4. Make sure that cold storage areas are not cooled to a lower temperature than is truly needed (refrigeration system energy use increases by 1% to 3% for every degree (F) of additional cooling).
  5. Make sure that products are not stacked directly under or in front of evaporators in cold storage units.
  6. Minimize other heat sources (such as lights and forklifts) in cold storage areas, which produce heat that must be removed by the refrigeration system.
  7. Report the formation of ice on cold storage area floors and walls. Ice indicates that a lot of air is entering the cold storage area, which carries moisture that gives off heat as it freezes, adding to the refrigeration load.
  8. Switch off system pumps and fans (such as those used for circulating cold air, chilled water, or anti-freeze) when not required. Pumps and fans can add significant heat loads to the refrigeration system during operation.
  9. Report and repair damage to refrigeration system pipe insulation.
  10. Regularly check compressor oil levels to ensure proper lubrication.
  11. Report and repair any refrigerant leaks.

Hi Industrial Energy Management - Fans & Blowers (Section 1).





Complete this questionnaire to better characterize the energy savings opportunities from Energy Management Systems. If an energy savings opportunity is identified, the results will appear immediately below the question.
Yes / No ?
  • Have you considered automatic on-off fan controls to reduce energy consumption?
  • Significant energy savings can be achieved by using an automatic fan control system to stop the fan when the ventilation is not required. Typical savings range from 10-50%. In addition to energy savings, this approach will reduce maintenance costs and increase equipment life.
  • Have you checked to see if all of your fans are properly sized?
  • Significant savings can often be achieved by selecting efficient fans that are sized as accurately as possible to work near their point of most efficient operation at the correct air flow. Fans that are properly sized for a particular application result in optimal energy consumption. However, it may often be more cost-effective to simply reduce the speed of the fan than to replace it. The rotation speeds on belt-driven fans can be changed by adjusting or changing the size and shape of the sheaves (pulleys). In this way, the fan speed can be optimized for fan efficiency and airflow, thereby reducing energy consumption. Typical savings range from 5-30% of fan energy consumption.
  • Have you considered improved controls and adjustable speed drives for fans that experience highly variable demand conditions to match the fan speed to the ventilation demand?
  • Ventilation demand often depends on the level of activity in the plant. As ventilation demand changes, an automatic controller can adjust the airflow rate to meet this demand, thereby saving energy that would otherwise be lost. The airflow rate can be adjusted using by using an adjustable speed drive (ASD) or variable pitch fan blades. Adjustable speed drive is just one of several terms used to describe a motor-driven system that rotates at variable speeds, such as variable speed drives (VSDs), adjustable frequency drives (AFDs), and variable frequency drives (VFDs). ASDs provide energy savings by matching the rotation speed to fan load requirements and thereby ensuring that motor energy use is optimized to a given application. ASDs can provide significant energy savings on fans that experience highly variable demand conditions. ASDs are best on fan systems that occasionally operate at low flow but do not operate for extended periods under low-flow conditions. For larger axial fans, adjusting the pitch of the blades is an alternative method for adjusting the airflow rate.
    Savings from ASDs and pitch controls can be as high as 30%. The resulting energy and maintenance cost savings can often justify the investment costs for the ASD. However, where there is no need to adjust the airflow rate, installing an ASD could increase energy consumption by 5%.
  • Have you considered straightening or turning vanes upstream of the fan inlet?
  • Significant savings can be achieved by making the airflow entering the fan more uniform across the fan. If there is swirl at the inlet that is moving in the opposite direction to the fan rotation, then fixed inlet vanes will straighten out the flow and provide fan energy savings. If there is a duct bend close to the inlet, then turning vanes installed in the duct bend will provide the fan with more uniform flow and provide energy savings. Typical energy savings is 5-15%.
    Similarly, it is generally good practice to not have ductwork bends close to the outlet. If there must be bends in the ductwork close to the outlet, use radius bends with splitters.
  • Is your ducting tubular with a large cross-sectional area?
  • Fan energy savings can be achieved by installing tubular ducting instead of standard rectangular ducting and ensuring that the cross-sectional area is as large as possible. The combination of large diameter and circular cross section will produce a low velocity system with a low pressure drop, thus maximizing efficiency. A duct that is too small for the required air velocity can significantly increase the amount of fan energy consumption. Where possible, duct diameters can be increased to reduce energy requirements, but the energy savings due to increased duct diameters must be balanced with increased costs for ducting system components. Increasing duct diameters is likely to be cost effective only during major system retrofit projects. Typical energy savings is 7%.
  • Have you checked to see if any of your fan motors are oversized?
  • Losses are often caused by the selection of a safety margin that is too large during the design and installation stages, resulting in the specification of a motor that is too large. Motors give good performance from 50-100% of rated load. Selection of the right motor is important. Typical energy savings range from 5-10%.
  • Has your company implemented a comprehensive fan maintenance program?
  • A comprehensive fan maintenance program will lead to fan system energy savings of anywhere from 2% to 7%. Inadequate maintenance can lower fan system efficiency and increase fan energy costs. The implementation of a fan system maintenance program helps to avoid these problems by keeping fans running optimally. A solid fan system maintenance program generally includes the following tasks:
    1. Cleaning dirty fan blades (dirt increases air drag which increases energy use and reduces the airflow rate, which requires higher fan speeds to maintain airflow rates and thereby increases energy use)
    2. Bearing inspection and repair
    3. Bearing lubrication replacement, on an annual or semiannual basis
    4. Inspection of motor condition, including the motor winding insulation
  • Have you installed high-efficiency belts (cog belts) where possible?
  • Belts make up a variable, but significant portion of the fan system in many plants. Cog belts are more efficient than standard V-belts. Standard V-belts tend to stretch, slip, bend and compress, which lead to a loss of efficiency. Replacing standard V-belts with cog belts can save energy and money, even as a retrofit. Cog belts run cooler, last longer, require less maintenance, and have an efficiency that is about 2% higher than standard V-belts. Payback periods range from less than one year to three years.
  • Have you considered adjustable speed drives on combustion air fans?
  • Often the cooling air and stack blowers run continuously, while variations in demand are either not met or they are met by using variable inlet vanes. The application of ASDs on the fan systems may be an opportunity for energy savings if there are variations in demand for air from the furnace. The savings (and hence payback period) will depend on the operating conditions of the fan system and the size of the furnace. One plant audit found electricity savings by installing ASDs on the furnace air blowers to have a payback period of 1.7 years. With large variations in heating demand (e.g., in small-scale intermittently used furnaces), installing an ASD may lead to savings in fuel use as well, as it reduces excess combustion air.
    The U.S. DOE’s Fan System Assessment Tool (FSAT) helps quantify the potential benefits of optimizing fan system configurations that serve industrial processes. FSAT requires only basic information about your fans and the motors that drive them. With FSAT, you can calculate the amount of energy used by your fan system; determine system efficiency; and quantify the savings potential of an upgraded system.


12 Mar 2013

Q-Flap Compact - II "A Donaldson Product Announcement."

Q-Flap Compact - II

For all Technical persons please be advised, this device is for ductwork installations. Available from Donaldson Torit DCE Product brought to you by Hammam Industries & Co. within the Middle East Region. 

REMBE Premium Explosive Protection, Designed to the New Testing Standard EN16447, Available in a range of Sizes of up to DN1000, Compare-sent made according to other simple back flap valve products for your acute reference. 



Calculate Your Cost Savings With Donaldson Tool Box Cost Saving Calculator for Energy Savings, Savings in Labor & Savings in Filter Bags Costs. 

"The choice of the filter media has an impact on the efficiency and economy of a dust collector. This tool will help calculate easily and quickly potential cost savings when your collector runs with Dura-Life filter bags" - Click Direct Link Here



26 Feb 2013

Hi CTI Journal, Vol. 31, No.1 - Cooling Towers, Drift, and Legionellosis.

Cooling Towers, Drift, and Legionellosis
CTI Journal, Vol. 31, No. 1



ABSTRACT

By itself, the presence of legionellae in a cooling tower is insufficient to predict the potential for disease transmission because other factors are involved.  This paper will describe details about one of the important factors, cooling tower air emissions, by providing a comprehensive technical understanding of drift quantity, droplet distribution, and plume dispersion.  By understanding these air emission details, ranges of Legionella bacteria concentration at distances from the tower can be estimated as a function of legionellae concentration in the tower water. This paper will also describe the ecology of the bacteria in cooling towers and the epidemiology of outbreaks attributed to cooling towers.  Most importantly, the paper will discuss the correlation of the bacteria-exposure model described in this paper with the incidents of disease from previously studied outbreaks. The quantity of bacteria required to cause disease depends on several factors including the health of the individual and the exposure.  A hypothetical example would be a situation where an individual could inhale 1 bacterium a week for fifty weeks with no ill effects, but develops disease when he inhales 50 bacteria in an hour.  There is likely some exposure rate (inhalation of X bacteria / time) where the risk of disease may occur; the higher the exposure rate, the more likely the occurrence of disease.  The inhalation rate (inhalation is the only means of transmission from cooling towers) depends strongly on two factors: 1) the concentration of bacteria in the ambient air in a particular area and 2) the time spent in that area.

INTRODUCTION

Legionellosis is a form of pneumonia caused from Legionella bacteria being inhaled or aspirated deeply into the lungs.  Legionella is quite common in the environment and there are many steps from
‘present in the environment’ to ‘disease’. The accepted prerequisite for infection is the bacteria must be contained in droplets of water less than 5 microns in diameter.  Larger droplets would not penetrate deeply enough into the lungs to cause infection.  While there is no known infectious dose or alternatively safe level for the bacteria, because of its ubiquity in nature, most researchers believe that an infection requires the inhalation of tens if not hundreds of bacteria.


As might be expected with the widespread distribution of Legionella bacteria, there is a ‘normal’, low incidence of random cases of Legionellosis.  With the low background rate, a cluster of disease would be statistically rare.  When a cluster has occurred, there is often a specific source identified as the cause of the outbreak. Outbreaks of community-acquired Legionella have been attributed to specific spas, fountains, cooling towers, metal working fluids, misters and other sources.  

With all of these sources except cooling towers, a very close proximity to the source was required for exposure.  With cooling towers, exposures have been reported several kilometers away from the purported source. The exposure to disease connection is not fully understood.  There are likely at least two competing processes occurring in the host: bacteria germination and host immune system response.  

In a healthy, non-smoking individual, an exposure of thousands of bacteria is likely necessary before the immune system is overwhelmed; in others the exposure of a few bacteria may be sufficient. It is not the norm for a cooling tower to cause an outbreak of Legionnaires’ disease.  There are hundreds of thousands of cooling towers in the US, many if not most containing some level of Legionella bacteria, yet there are only a handful of cooling-tower implicated outbreaks.  A person’s exposure to Legionella bacteria from a cooling tower is based on a variety of factors:

1) The drift rate of the tower.  Drift is the mechanically aspirated droplets of circulating water that are en trained into the effluent air stream.
2) The volume of air passing through the tower.
3) The dispersal of the exhaust air with ambient air (plume dilution).
4) The time spent in plume/air mix
5) The concentration of Legionella bacteria in the circulating water.

This paper will explore these factors and the effect they have on
risk of exposure.

COOLING TOWER DRIFT

Most tests on a specific tower design show a linear relationship between circulating water flow and drift within normal cooling tower operating air flow.  Air flow rate will significantly affect tower drift
only at the extremes of the design.  Because of this, drift is typically described as a percentage of circulating water rate. All modern cooling towers are or should be equipped with drift eliminators (DE).  The DE force the exhaust air to make sharp turns before exiting.  

The momentum of en-trained droplets carries the droplets to the DE surfaces where they coalesce and drip back into the tower.  Cooling towers or drift eliminators may be evaluated for drift rates under controlled conditions.  The standard test is the “Heated Bead Isokinetic (HBIK) Drift Test Procedure” described in the Cooling Technology Institute code ATC 1401.  A portion of the exit air stream is drawn at the same speed and direction (isokinetically) into a collection device.  The collection device consists of heated beads.  Any drift that is pulled into the tower is dried on the beads. 

The tower water has a specific concentration of a tracer element and by measuring the quantity recovered from the beads, the quantity of drift can be determined. Less modern designs for drift eliminators are not as efficient as newer equipment.  While an older design might result in drift rates up to 0.02%, all towers constructed in the last few years by the major manufacturers are much better.  Typically, for cross-flow designs the drift rate will be less than 0.005% while because of use of higher efficiency eliminators, counter-flow designs routinely achieve 0.001%. 

The newer cellular drift eliminators started being used in the late 1980’s with particular model lines changing over about a 15-year period.  Around the early 1990’s the 0.005% drift rate for cross-flow towers became standard.  The 0.001% drift rate for induced-draft counter-flow became standard also around 1990.  For forced-draft counter-flow units, 0.001% didn't become standard until just a few years ago.  Prior to the change, cooling tower drifts were typically

in the 0.02% or higher range. A typical 1,000-ton HVAC cooling tower nominally circulates 3,000
gpm water.  At nominal conditions, the drift from a 1,000-ton cross-flow tower would be less than 0.15 gpm while the drift from a 1,000-ton counter-flow tower would be less than 0.03 gpm.  These values should be routinely achieved by units as they are shipped from the factory.  With a well maintained tower, these rates can be sustained for many years.  However, there are things that happen in the field which can degrade the eliminators effectiveness.  

A partial list of these problems follows:

1) Damaged drift eliminators.  UV, hail, and improper handling can all damage drift eliminators.  Damaged drift eliminators interfere with exhaust air flow.  If there are gaps or holes in
the eliminator, then more air will pass through the open area at high velocity carrying significantly more en-trained water.

2) Clogged drift eliminators.  In highly cycled water the entrained droplets contain a high quantity of dissolved solids.  This can result in a gradual build up of minerals on the DE.  As the minerals build up, the air is blocked in some areas and the air velocity increases in the open areas.  As this velocity gets high enough, the amount of entrained water carried from the tower increases.

3) Misaligned or missing drift eliminators.  If there are gaps in the eliminators, their effectiveness is severely reduced.

4) Damaged fill.  While not as obvious as damaged drift eliminators, damaged or partially clogged fill will change the airflow to the DE and affect their efficiency

5) Obstructed inlet air.  For the same reason as in #4, changing the airflow in the tower affects DE efficiency.

6) Water distribution.  Improper water distribution may put too much water in one area resulting in very high drift from that part of the tower. Misaligned or over-pressured spray nozzles can also increase the amount of drift.

7) Use of surfactants in the chemical water treatment. By lowering the surface tension of the recirculating water, surfactants can cause water to form very small droplets. These small droplets are more easily carried by the air stream and are less effectively removed by the drift eliminators.

The drift that leaves the tower is in the form of small droplets. 

The larger the droplet the more momentum it carries and the more effective the DE. The distribution of water drop sizes in the drift can be measured by water sensitive paper. 

The paper is treated so that a droplet impinging on the paper will generate a well defined mark. The size of the stain is related to drop size 2 . This is a less exact method than the HBIK test but provides some information about droplet size distribution. This test is not effective for droplets less than 30 microns in size. 

Many studies have been performed on the size of drift particles from a tower. Figure 1 shows the results from nine separate tests on drift eliminators performed by the manufacturer. The cumulative volume of drops is plotted as a function of the diameter of the drop in microns. Below each label on the X-axis is the number of droplets of that specific diameter per milliliter of water. 

The drops per ml information is useful to see that, absent clumping, it would be very unusual for a single droplet to contain more than 1 Legionella bacterium even in a heavily contaminated system with a Legionella count per ml of 1,000. Because of this, parametric statistical analysis is valid for considering Legionella dispersion in the plume.


Figure 2 displays results from another droplet distribution test performed on two towers in-the-field 4.  Also include in Figure 2 is a line at the 50 micron drop size.  A 50 micron diameter particle is
1000 times larger than a 5 micron respirable particle.  Droplets larger than this line are at least 1000 times larger than respirable size. Most of the volume of the drift as it leaves the tower is in droplet
sizes too large to be deeply inhaled.  The bacteria contained in those droplets can cause disease only if the droplets evaporate to a respirable size before falling to the ground.

CONCENTRATION OF LEGIONELLA  IN COOLING TOWER EXHAUST

Cooling towers cool water by evaporation, thereby exchanging both heat and humidity to the air.  The amount of air passing through a tower per gallon of water depends on both the design of the tower
and often on the heat load on the tower for towers equipped with multispeed fans. 

The design mass flow rate of circulating water to cooling air is usually given as an l/g ratio with the both the liquid and gas amounts given in pounds.  A quick review of manufacturer catalogs shows that induced-draft counter-flow towers are designed with an l/g ratio between 1.43 and 2.23.  

Induced-draft cross-flow towers are designed with a lower l/g ratio of between 1.34 and 1.50.  Both designs produce an equivalent amount of cooled water per fan HP, the counter-flow run lower air volumes at slightly higher pressure than cross-flow towers.  

Forced-draft counter-flow towers typically run at range of l/g ratios between 1.10 and 1.65.  Using a nominal specific volume of air of 14 cubic feet per pound, Table 1 shows the min and max concentration of drift in the exhaust air at the referenced drift rates.  This value is then extrapolated to a nominal time that an individual would need to breathe undiluted cooling tower exhaust to, on average, inhale a single Legionella bacterium.  

The values in Table 1 are based on full fan power.  It is assumed that the drift rate as a percentage of the circulating water rate does not fall appreciably until the fan rate drops below 50%.  Thus for low fan speeds, the concentration of drift, and hence Legionella bacteria, could be up to twice as high as is shown in the table. 

In 1988 there was a Legionella outbreak at a Los Angeles retirement home 5 .  The investigation of that outbreak identified a below ground forced-draft evaporative condenser as the source of the outbreak.  While the specifics of the condenser were not included in the paper, Table 1 contains calculations using a typical evaporative condenser with 1988-style drift eliminators.  

The investigation measured Legionella in the tower basin of 9,000 CFU/ml.  The investigation also used impinger sampling data to estimate that there were 2.3 CFU/liter of air of Legionella in the condenser exhaust vent.  That 2.3 CFU/l agrees very closely to the 2.8 CFU/liter that was calculated using the approach of Table 1.

PLUME DILUTION 

Only a very small percentage (on the order of 1%) of the drift as it leaves the cooling tower is of respirable size, and hence able to cause an infection.  The remainder of drift and contained Legionella consists of droplets greater than 5 microns.  

Thus a person breathing undiluted exhaust air from a well-maintained cooling tower with what might be considered a moderate concentration (100 CFU/ml) of Legionella would need to be in the exhaust much longer (possibly 99 times longer) than the times indicated in Table 1 before he statistically would inhale a single Legionella bacterium deeply into his lungs.  

The droplets can evaporate to respirable size once they travel a distance from the tower. When exhaust air leaves a cooling tower it forms a plume.  The characteristics of this plume depend on a complex interaction of, among-st others, the following:

1. wind speed and direction
2. buildings and structures down wash
3. buoyant/dense plume behavior
4. gravitational settling
5. droplet evaporation and humidity condensation (phase changes)
6. surrounding terrain
7. ambient temperature and humidity 

Because of the complexity of the flows around the cooling equipment we will not focus on the ‘near-field’ plume.  In addition, the water droplets in this area are likely too large to inhale deeply into the lungs.  We are defining this near-field to extend 20 fan diameters from the base of a tower.  

This is the approximate distance that the plume from a ground-level tower would reach the ground under the simplified plume dispersion model shown below. There are several computational fluid dynamic programs that attempt to model plume behavior with varying success^6.  Beyond some generalizations, the detailed prediction of cooling tower plume is beyond the scope of this paper.

With the previous caveat, there are some generalities that can be stated.  For the basic condition we will assume that people are all located at ground level.  The worst case scenario would then be a tower installed on or near the ground. One of three things can happen as the ambient air mixes with the cooling tower exhaust air^7:

1. If the air is very still, the exhaust may climb very high and be dispersed over a very large area before it reaches ground level.

2. If the ambient air is very turbulent, winds greater than 20 mph, the plume will be rapidly diluted and dispersed.

3. The third condition is a steady mild breeze of 5 to 10 mph. This condition is sufficient to bend the plume over and bring it to ground level, yet the plume will maintain some cohesiveness. This is the condition that will most likely bring a person in contact with contaminates from the cooling tower and is the condition that we will discuss in the remainder of this section.



SIMPLIFIED PLUME DISPERSAL MODEL – Under mild winds, plumes will generally expand in both the height and width direction with a typical angle of expansion of approximately 6.0°.   A simplistic model of a cooling tower, sitting on the ground with a unit discharge characteristic dimension ‘F’ (this will be approximately equal to the fan diameter on an induced-draft tower) is shown in Figure 3.  

The plume is dispersed from an area equal to the discharge characteristic dimension squared (F2).  As the plume spreads, the concentration of the cooling tower exhaust is diluted by the ratio of the cross-sectional areas.  When the plume touches the ground, the plume expansion changes from a square to a rectangle since the ground blocks the plume from further downward expansions.  The model is particularly inaccurate in the ‘near field,’ before the plume touches the ground.  This area is essentially being ignored because the drift droplets as they leave the tower are too large to be respirable. 

Time and distance are required for the droplets to be reduced to 5 microns or less in size.  For modeling Legionella dispersion in the far-field, we assume, conservatively, that all Legionella bacteria are in respirable-sized droplets. Due to the momentum of exhaust air as it leaves the tower, the plume will tend to rise up before bending down.  To account for this rise, the height of the plume when it bends is set at twice the characteristic discharge dimension.  For typical factory-assembled, HVAC cooling towers set on the ground this is a reasonable assumption.

Figure 3 details the near-field plume dispersion of the simplified model.  With this model, the plume touches the ground at a distance D0 = 2F/ tan (6 o) = 20 F.  At this point the cross-sectional area of the plume will be (5F)^2, 25 times the area as the plume left the tower.  We are calling this D0 the characteristic distance and using multiples of this distance as a simplified way to describe plume dilution independent of cooling tower size.



We have arbitrarily set the point where the plume touches the ground, D0 , as the end of the near-field.  As the plume continues to expand beyond this point, it is constrained from expansion in the vertical direction by the ground.  We assume no such constraint in the horizontal direction.  

Figure 4 illustrates how these assumptions affect the plume dilution. At 2x D0 the cross-sectional area is 63 F^2, at 3x D0 the area is 117 F^2 , and at 4x D0 the area is 187 F^2 .  

The ratio of the cross-sectional area of the plume at a specific distance to the cross-sectional area of the plume as it leaves the tower (F^2) is a measure of the dilution of the cooling tower exhaust by ambient air at that point.




The characteristic distance, D0, that the plume travels before it touches the ground is a function of the discharge dimension.  Larger units exhaust higher off the ground and the near-field of the plume extends for a greater distance.  Table 2 lists this distance for some common sized units used in factory-assembled towers as well as some multiples of this distance.


COMPARISON OF SIMPLIFIED MODEL WITH EPA SCREENING MODEL – The EPA has several plume modeling programs for estimating air quality impact of stationary sources.  One of these programs, SCREEN3^8, was used to validate the simple model described in this paper.  

Data was input for ground level pollutant dilution from two cooling towers, one with a 12-foot diameter fan and operating at ½ fan speed; the other with an 8-foot diameter fan operating at full speed.  The program automatically chooses the wind and atmospheric conditions that produce the highest concentration at a given distance.  

From these worst-case concentration values, the plume dilution was calculated.  The values of the SCREEN3 worst case dilutions are plotted against the simplified model dilutions in Figure 5.  There is very good agreement between the two models.

Both these models assume no other structures in the immediate area.  The close agreement of the simplified model with the EPA model helps to validate the reasonableness of this simplified approach.
The simplified model allows a quick consideration, independent of tower size, of the plume dilution at a distance from the tower.  The model fails at very short distances (less than 20 fan diameters the
simplified model assumes zero ground-level concentration) and at very long distances.  For the intermediate distance in an open area it has some use.

BACTERIA CONCENTRATION IN PLUME

We can now combine the bacteria concentration in the drift from Table 1 with the plume dilution after it touches the ground from Figure 4 to determine how many hours someone must be at several
distances from the tower in order to, on average, inhale a single Legionella bacterium.

These calculations assume:

1. A mechanically well-maintained tower (drift eliminators, fill, nozzles, etc.)
2. A moderate Legionella contamination of the circulating water of 100 CFU/ml
3. Ground-level tower (worst-case)
4. The worst-case l/g (at full speed) for typical modern cross-flow towers and for typical modern counter-flow towers (in terms of drift concentration in the cooling tower exhaust).

5. Fans operating at ½ speed (worst-case doubling the drift concentration from full fan speed).


6. All of the Legionella bacteria that leave the tower become respirable (worst-case).

Table 3 indicates that in a modern tower that was acceptably maintained there is little chance of inhaling multiple Legionella bacteria unless one spent extensive time close to the tower under a worst scenario wind condition or if the cooling tower were sited very near a building fresh air intake.


LEGIONELLA IN COOLING TOWER WATER

THE ECOLOGY OF LEGIONELLA – Legionella have a unique ecology compared with other bacteria that live in water.   It is now well understood that Legionella in the environment grow as intracellular parasites of free-living amoebae and other protozoa. Rowbotham9 first demonstrated the ability of Legionella to replicate within freshwater and soil amoebae as early as 1980, and since then this phenomenon has been confirmed by many investigators using Acanthamoeba, Naegleria, and Hartmanella amoebae, and the ciliated protozoan Tetrahymena 10. Most authorities agree that this intracellular replication not only plays a vital role in the amplification of Legionella in the environment, but is also the unique pathogenic ability that enables Legionella to infect humans via the intracellular replication with monocytes and macrophages.

In an environmental habitat such as a cooling tower, most of the amoebae reside as part of the biofilm on the solid surfaces, rather than free in the water.  This complex ecosystem contains a wide variety of slime-producing bacteria that colonize the surfaces, along with higher organisms such as amoebae and other protozoa that graze on the bacteria as a food source. 

Legionella interact with the amoebae in the biofilm, blocking the killing and digestion process of the amoebae, and replicating to large numbers within the food vacuole or vesicle inside of the amoebae. Eventually the amoeba is killed and the Legionella are released to find new hosts.  Some of the bacteria (including Legionella) and amoebae in the biofilm migrate from the surface into the free-flowing water and are distributed to other biofilm locations.  

It is these water-borne (referred to as planktonic) Legionella, along with other bacteria and amoebae, that are released into the air from the cooling tower in the drift. Rowbotham8,11 has described the replication cycle of Legionella within the amoebae and first noticed the release of small vesicles full of Legionella at certain stages.  He hypothesized that, while intact amoebae (10-40 ìm diameter) are generally too large to be inhaled into the lungs, the inhalation of small (<5 ìm) vesicles packed with  Legionella could provide an infectious dose in a single inhalable particle 10. 

More recently, Berk and colleagues 12 have more convincingly demonstrated the production of respirable vesicles (2-6 ìm in diameter) containing live Legionella from Acanthamoeba. Berk 11 estimated that each vesicle could contain between 20 and 200 bacteria, while Rowbotham10  calculated numbers in the range of 365-1,483 Legionella for a 5 ìm diameter vesicle.  These membrane bound vesicles would also protect the Legionella from desiccation during the airborne dissemination from the tower. 

Thus, from a disease transmission perspective, the cooling tower drift that exits the tower would contain a mixture of free Legionella, clusters of Legionella within respirable amoebae vesicles, and intact amoebae containing Legionella.  In would seem obvious that the respirable vesicles would provide the highest risk to humans since they can be inhaled into the lungs, with a single vesicle providing a potentially infectious dose of Legionella.

THE STANDARD CULTURE METHOD FOR LEGIONELLA – The gold standard for detection and quantitation of Legionella in cooling towers or other environmental water samples is the standard culture method originally described by the CDC13. In this procedure, samples (with and without acid treatment to reduce the other heterotrophic bacteria in the water) are diluted and portions plated on selective and non-selective agar media.  Any Legionella-like colonies that appear after appropriate incubation are confirmed as Legionella (species and serotype) with standard confirmation procedures.  Using the assumption that each colony originated from a single bacterium, the number of Legionella in the water can be calculated and recorded as “colony forming units” (CFU) per ml or liter of original sample.  

To date, a number of organizations have published protocols for the culture of Legionella from environmental samples including an international standard (ISO 11731) 14. Culture of Legionella from environmental samples is technically demanding and successful testing requires a microbiology laboratory that is experienced in the detection of this bacterium.   There are no programs to certify the proficiency of environmental laboratories for their ability to culture Legionella.  

In addition, variations which can be associated with procedures such as filter concentration or acid pretreatment (to kill non-Legionella bacteria) can dramatically affect the number of  Legionella detected by these procedures.  CDC will be initiating a proficiency testing program for environmental laboratories culturing Legionella in 2009 which should help with the standardization of these practices.  Until that time, the only way to ensure accurate testing results is to rely on highly experienced laboratories. 

It should be noted that other non-culture techniques are available for detection and quantitation of  Legionella in environmental samples, including antigen-antibody based methods (such as immunofluorescence microscopy) and nucleic acid detection procedures such as polymerase chain reaction (PCR).  The major limitations of these other procedures is that they may cross-react with other bacteria in the water and do not distinguish between living (infectious) and dead (non-infectious) Legionella in the sample.

LEGIONELLA CONCENTRATION IN TOWER WATER – Using the standard culture technique, many investigators have shown that Legionella is a common part of the microbial ecosystem in cooling tower water, although usually at low concentrations.  

Results of a large survey of cooling towers (2,590 samples) over several years published by Miller and Koebel in 2006 15 showed that 12% of the tower samples had detectable Legionella above the limit of sensitivity of 10 CFU/ml and 2% of the samples had levels above 1,000 CFU/ml.  

A similar Spanish study presented at the European Congress of Clinical Microbiology and Infectious Diseases in 2004 by Garcia-Nunez 16 found that 18 % of 554 cooling towers randomly sampled over a three-year period were culturepositive for Legionella at their increased limit of sensitivity of 10 CFU/liter.  

Legionella numbers generally constitute a small percentage of the total bacterial population in tower water (usually < 1% of the total heterotrophic bacteria).  However, Miller and Kenepp 17  showed that (perhaps as a result of biocide selectivity), the Legionella numbers may occasionally approach or achieve 100% of the bacterial population in the cooling tower water, often at levels exceeding 1,000 CFU/ml.   

Cooling towers responsible for outbreaks of Legionnaires’ disease often have high concentrations of Legionella in their water.  To the best of out knowledge, the highest concentration reported in such an outbreak investigation was in a tower which contained 10 5 CFU/ml of L. pneumophila 16. Analysis of cooling tower water with non-culture methodology tends to give higher percentages of samples positive for Legionella. 

This is due to 1) the detection of both living and dead Legionella in the samples, and 2) the increased sensitivity of PCR over the standard culture method (i.e. the ability to detect very low levels of Legionella in the sample). 

UNDER ESTIMATIONS OF THE STANDARD METHOD – While the standard culture technique is generally very reliable and reproducible in a qualified laboratory, this method may significantly under-estimate the actual number of Legionella in a cooling tower water sample as a result of:

1.  Interference by other bacteria.  Because Legionella is usually a minority of the total bacterial population in the cooling tower water, it is essential that the acid treatment and selective media successfully eliminate or inhibit the other bacteria so that the Legionella can grow without interference.  While occasionally encountered in all labs, interference is a problem most common in laboratories not familiar with these critical elements of the standard procedure.

2.  Viable but non-culturable (VBNC) Legionella.  Examination of cooling tower water by non-culture techniques such as immunofluorescent microscopy or polymerase chain reaction (PCR) often reveal the presence of  Legionella in samples that were culture-negative, or higher numbers of Legionella in samples that were culture-positive.  The demonstration of a VBNC state for Legionella has been convincingly demonstrated by several investigators using nutrient limitation 18,19,20  or disinfectant exposure 21,22.  These VBNC Legionella can be resuscitated by exposure to amoebae and are potentially infectious for humans.

3.  Clusters of Legionella bacteria.  Any clusters or clumps of Legionella introduced onto an agar plate would form a single colony and be under-counted as a single Legionella bacterium.  Clusters containing more than one Legionella are readily observable when water samples are examined using immunofluorescence microscopy (IFM).  

If each cluster were counted as a single Legionella, the clusters may account for as much as 5-10 % of the Legionella observed by IFM (personal observation).  Additional clusters of Legionella within intact amoebae or amoebae vesicles may not be observed by IFM due to an inaccessibility to the anti-Legionella antibody used in this method, but still form single colonies when cultured onto an agar plate.  

Thus, the production of vesicles (each containing potentially large numbers of viable Legionella) by amoebae or other protozoa would be of great importance in terms of disease transmission.

EPIDEMIOLOGY OF OUTBREAKS

The preceding sections have discussed a semi-quantitative methodology for evaluating the risk for a Legionella infection from a cooling tower.  The fundamental question is does the epidemiology data support the methodology.

The methodology assumes that the concentration of airborne bacteria is due primarily to four factors:

1. The concentration of Legionella bacteria in the circulating water.
2. The quantity of drift generated by the tower.
3. The quantity of air passing through the tower.
4. The dilution of the plume by ambient air. 

The exposure dose and hence the risk of disease is then related to the time spent breathing in the contaminated air. Robert Breiman^5 describes a 1988 outbreak at a Los Angeles retirement home.  The data from that study was used to validate the methodology used in Table 1 for calculating the concentration of Legionella bacteria in cooling tower exhaust.  The cooling system consisted of a below ground, forced-draft evaporative condenser that exhausted at sidewalk level.  There was an air intake to the building located near and slightly higher than the exhaust.  Tests on the water in the condenser basin showed Legionella counts of 9,000 CFU/ml.

The cooling system in that study had many problems with its design and operation that are addressed with current guidelines.

1. The drift eliminators on modern counter-flow towers are 20 times better.  This alone may have prevented the outbreak. 

2. 9,000 CFL/ml is very high.  Almost any good water treatment would lower this value by one to two orders of magnitude.

3. The location of the building inlet air was particularly bad. Cooling tower exhaust always has some buoyancy and will usually rise as it leaves the tower.  Locating the building air-inlet near and above the exhaust is particularly bad.

4. Exhausting an underground condenser at sidewalk level is improper.

5. Towers sited on the ground have a tendency to draw in a broad array of organic and mineral contaminates – much more so than a tower sited on a roof.  An underground tower that draws its inlet air downwards is even more likely to draw in contaminates.  These contaminates make biological control of the circulating water more difficult.

6. Since this is a retirement home, it would warrant special attention An order of magnitude analysis of the condenser identified as causing the out break show that the drift rate was an order of magnitude
too high, the bacteria concentration in the recirculating water was two orders two high, and the location of the condenser exhaust and the building air intake resulted in a order of magnitude more contaminated air being drawn into the building.  Had any one of the order-of-magnitude criteria conditions been properly controlled, the probability of an outbreak would have been greatly reduced. Clive Brown^23 describes a 1994 outbreak in the area around a Delaware hospital.  The paper strongly suggested a relationship to time spent near the contaminated cooling tower and risk of infection.

The authors develop a variable which they call an Aerosol Exposure Unit (AEU) to describe the dose that an individual received. The AEU is proportional to the hours spent at a specific distance
from the tower with a formula of:

AEU = time (in hours) / distance (in miles).

The authors performed a detailed case-control study of 22 people who came down with the disease and matched controls of similar age and health that attend the same clinic but were disease-free. This study showed a very strong correlation with high AEU and disease. 

The AEU formula assumes that:

1. The dose is linear with time spent breathing contaminated air.  This is exactly the assumption that we are making.

2. The contamination falls off in a linear manner the farther the distance form the tower.   The AEU formula implies that contamination-concentration is proportional to 1/distance. Since contamination-concentration is proportional to 1/ plume-dilution, the AEU formula assumes a linear increase between plume-dilution and distance. This is different from the model used in this paper. 

Our model assumes a quadratic increase in plume dilution with distance.  Although different, the result on this relatively small data base may not be noticeable.  

Figure 6 is a plot of the plume dilution of a ground-based tower with a 12’ fan using the model proposed in this paper.  Also on this plot is a linear regression of those points that is forced through the origin.  This linear regression represents the relationship used to develop the AEU variable.  The difference in the two plots is not likely to be significant in the disease-AEU correlation.

DISCUSSION

This description of Legionella concentration in a dispersed plume is only intended as an order-of-magnitude approximation.  While there is no known safe levels of Legionella exposure, values that are less than 1 Legionella bacterium inhaled in 24 hours seem very low.  This indicates that if current guidelines are followed – good drift eliminators, good mechanical repair of the tower, sound tower sitting practice, reasonable microbiological control, etc. – the risk of Legionella infection can be quite low.

The basic plume dispersion model is a very simplified case.  Buildings in the area of the tower as well as other structures will dramatically affect how the plume is diluted.  The simplified model is only
intended as a visualization and order-of-magnitude approximation that bacteria concentration, in general, decreases as distance from the tower increases. There are well-documented cases of Legionellosis associated with cooling tower exposure – how does this analysis help understand those cases?  In general, two or more of the basic assumptions of this analysis were not followed.  It is useful to review the basic assumptions of this analysis because they certainly do not apply in many situations.  The assumptions of this analysis are:

1. That modern drift eliminators (0.005% for cross-flow and 0.001% for counter-flow  are being used.  The drift eliminators that were the standard just a few years ago were much less effective, having drift rates up to an order of magnitude higher.

2. That the tower is in good mechanical shape.  Damaged or missing drift eliminators will greatly increase the level of drift.  While much of the drift from such a tower will be in very large, rain-drop sized drops that fall quickly to the ground, some will be en-trained in the air and contribute to
the respirable Legionella loading of the plume.

3. The tower is assumed sited on a clear area of ground with people below the level of the exhaust.  A subterranean installation with a ground-level exhaust would be more dangerous as would locating the cooling tower such that the exhaust can be drawn into a building’s air inlet.

4. Reasonable water treatment is in effect.  Although not specifically aimed for Legionella eradication as is required by some non-US regulations, water treatment that keeps good general biological control is assumed.

Another underlining assumption is that infection is caused by the inhalation of individual Legionella bacteria.  As previously described in this paper, there may be vesicles in cooling towers which may contain tens if not hundreds of Legionella bacteria.  The cooling towers in the outbreaks discussed in this paper all had old-style drift eliminators, high levels of Legionella in the basin, and were improperly sited.  The contamination level was sufficiently high to allow an individual to inhale tens if not hundreds of Legionella bacteria by spending a relatively short time in the tower plume. 

These outbreaks can be explained by inhalation of sufficient individual bacteria to cause a disease.  However, these outbreaks could also be explained by the inhalation of individual vesicles emitted in the drift. There are several studies 24,25,26 that implicate a cooling tower with infection that occurred at a considerable distance from the cooling tower.  A vesicle-vector would help explain how an infectious dose could be inhaled at a significant distance form the tower. 

If vesicles are the disease vector, and if a single vesicle contained sufficient Legionella bacteria to provide an infectious dose, then the analysis would change.  A very simplified example illustrates the difference. If we had an aerosol contamination such that there was 1 chance in 10 that a person would inhale 1 bacteria in a minute and 1000 people spent 1 minute breathing the air then 100 people would breath in 1 bacteria.  A single bacteria is probably too low a dose to cause disease so nobody gets infected.

If we had an aerosol contamination such that there was 1 chance in 100 that a person would inhale 1 vesicle in a minute and 1000 people spent 1 minute breathing the air then 10 people would inhale a
vesicle.  If every vesicle contained a large quantity of bacteria then some of the 10 could become infected, depending on the health of the individual.

Current epidemiological data has not been able to distinguish between the alternative vectors and it is possible that both vectors are involved in infections.  Reduction or elimination of vesicles in
tower water could require a different water treatment approach than reduction of Legionella bacteria.

CONCLUSION

There are many excellent guidelines for minimizing the risk of Legionella infection from cooling towers.  These guidelines all recommend proper maintenance, good drift eliminators, proper siting, and good biological control among many other recommendations; however, none of these guidelines attempts to describe the relative importance of these recommendations. Because of the quantitative nature of biological control, that aspect is often emphasized over other aspects of control.  A 1990- genre cooling tower with drift eliminators that reduce drift to 0.02% and a Legionella count of 50 CFU/ml might be thought of being a low risk of infection while a 2000-genre cooling tower with drift
eliminators that reduce drift to 0.001% and a Legionella count of 1000 CFU/ml would require immediate disinfection.  

Using the approach in this paper, the 2000-genre cooling tower presents a similar risk for a community-acquired infection than the less contaminated, older tower.  One way to reduce the risk of Legionella exposure from older equipment is to upgrade the drift eliminators to the modern, high-efficiency designs.

Further studies of the transmission vector for cooling-tower infection (bacteria, vesicles, or both) are needed.  The control of amoebae and vesicles in the cooling water may require different water treatment than the control of planktonic Legionella bacteria.  

The factor that vesicles may play in disease transmission needs to be better understood. It has been well known that the level of Legionella bacteria in the cooling tower plays some role in the risk of infection; however, the mere presence of the bacteria is insufficient to predict the potential for disease transmission.  The semi-quantitative approach to Legionella aerosol exposure level, as outlined in this paper, can be very beneficial in the management of several of the differing factors that contribute to risk of Legionnaires’ disease transmission.  

The importance of drift eliminator design, physical maintenance practices, and siting as well as bacteria counts can all be roughly weighed as to their contribution to the overall risk-of-infection.  The authors
feel that the semi-quantitative approach taken in this paper can be beneficial in evaluating the risks associated with a particular cooling tower, evaluating the benefits of proposed changes in cooling tower guidelines, evaluating the importance of equipment design modifications, and aiding in the investigation of outbreaks.

REFERENCES

CTI Journal, Vol. 31, No. 1





Hi Blog List.

Hi Translate.

Hi Smoke Poll, User Star Rating!.

Hammam Industries & Co.

Hammam Industries & Co.
'Regional MESAN CTI Certified Cooling Towers Suppliers'

The Hi European Commission.

The Hi European Commission.
"The Latest EU Industry Regulations Information".

Hi Wikipedia Search.

Search results

Hi Blogger Contact Form.

Name

Email *

Message *

Hi Revenue Slider